JP2001328807A - Method of purifying quartz powder and product made of quartz powder - Google Patents

Method of purifying quartz powder and product made of quartz powder

Info

Publication number
JP2001328807A
JP2001328807A JP2001019768A JP2001019768A JP2001328807A JP 2001328807 A JP2001328807 A JP 2001328807A JP 2001019768 A JP2001019768 A JP 2001019768A JP 2001019768 A JP2001019768 A JP 2001019768A JP 2001328807 A JP2001328807 A JP 2001328807A
Authority
JP
Japan
Prior art keywords
quartz powder
quartz
container
refining
powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001019768A
Other languages
Japanese (ja)
Other versions
JP4557441B2 (en
Inventor
Masaharu Ishiwatari
正治 石渡
Toshio Tsujimoto
俊夫 辻元
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Corp
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Filing date
Publication date
Application filed by Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP2001019768A priority Critical patent/JP4557441B2/en
Publication of JP2001328807A publication Critical patent/JP2001328807A/en
Application granted granted Critical
Publication of JP4557441B2 publication Critical patent/JP4557441B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C1/00Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
    • C03C1/02Pretreated ingredients
    • C03C1/022Purification of silica sand or other minerals

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Melting And Manufacturing (AREA)
  • Silicon Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a purification process and an apparatus therefor which can efficiently remove the metal impurities from quartz powder with simple constitution. SOLUTION: A purification vessel that is equipped with a partition wall made of quartz glass between the anode and the cathode is used to form an electric field in the quartz powder charged on both sides of the partition wall under high temperature whereby the metal impurities are allowed to move toward the anode side and the metal impurities is lowered in the quartz powder on the cathode side.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、石英粉末に含まれ
るアルカリ金属や鉄、銅などの不純物金属量を低減する
精製方法と装置および精製した石英粉末を用いた製品に
関する。より詳しくは、半導体工業用石英ガラス材料、
シリコン引き上げ用石英ルツボ等の原料として用いられ
る天然石英粉末等の精製技術に関する。
The present invention relates to a purification method and apparatus for reducing the amount of impurity metals such as alkali metals, iron, and copper contained in quartz powder and products using the purified quartz powder. More specifically, quartz glass materials for the semiconductor industry,
The present invention relates to a technique for purifying natural quartz powder and the like used as a raw material for a quartz crucible for pulling up silicon.

【0002】[0002]

【従来の技術】天然石英には微量のアルカリ金属が含ま
れている。このアルカリ金属を含有する石英粉末を石英
ガラスルツボ等の半導体工業用の熱処理部材等に使用す
ると部材の変形や失透を生じる。また、シリコン単結晶
の引き上げに用いる石英ガラスルツボの場合には、ルツ
ボに含まれるアルカリ金属によってシリコン単結晶が汚
染される問題がある。そこで、天然石英等からアルカリ
金属不純物を除去するために、(イ)電場を印加してアル
カリ金属を陰極側に濃集させる方法や、(ロ)高温下で塩
素含有ガス等を導入し、アルカリ金属を塩化物にして揮
発除去する方法などの精製法が従来から知られている。
2. Description of the Related Art Natural quartz contains a trace amount of alkali metal. When the quartz powder containing the alkali metal is used for a heat treatment member for the semiconductor industry such as a quartz glass crucible or the like, the member is deformed or devitrified. In the case of a quartz glass crucible used for pulling a silicon single crystal, there is a problem that the silicon single crystal is contaminated by an alkali metal contained in the crucible. Therefore, in order to remove alkali metal impurities from natural quartz or the like, (a) a method of applying an electric field to concentrate the alkali metal on the cathode side, or (b) introducing a chlorine-containing gas at a high temperature, etc. A purification method such as a method of converting a metal into a chloride to volatilize and remove the metal has been conventionally known.

【0003】例えば、特開昭59-129421号公報、特開昭6
0-137892号公報、および特開平06-16494号公報には、石
英インゴットないし石英ガラスルツボ製品に、1200
〜1300℃の加熱下で、10〜50kvの直流を印加す
ることにより、製品中のアルカリ金属イオンや銅イオン
を移動させることが記載されている。しかし、これらの
電解精製法はガラス製品に関するものであり、石英粉末
についてそのまま適用するのは難しい。ガラス製品の場
合は製品表面に電極を装着して通電することにより製品
の一部にアルカリ金属を濃集させることができるが、石
英粉末では粒子が流動化するので、石英粉末に通電して
アルカリ金属を陰極側に濃集させても、通電後に石英粉
末を取り出す際に、陰極側と陽極側の石英粉末が混じり
合うと十分な精製効果は得られない。
For example, JP-A-59-129421 and JP-A-6-129421
JP-A-137892 and JP-A-06-16494 disclose a quartz ingot or a quartz glass crucible product of 1200
It is described that an alkali metal ion or a copper ion in a product is moved by applying a direct current of 10 to 50 kv while heating at a temperature of 11300 ° C. However, these electrolytic refining methods relate to glass products, and it is difficult to apply them directly to quartz powder. In the case of glass products, an alkali metal can be concentrated on a part of the product by attaching electrodes to the product surface and energizing it.However, particles of the quartz powder are fluidized. Even if the metal is concentrated on the cathode side, a sufficient refining effect cannot be obtained if the quartz powder on the cathode side and the quartz powder on the anode side are mixed when the quartz powder is taken out after energization.

【0004】一方、石英粉末については塩素含有ガス等
を用いた精製方法が従来知られている。例えば、特開昭
55-42267号公報、特開昭62-30632号公報、特開昭63-100
038号公報には、天然石英粉末等を塩素含有ガス流中で
加熱処理することにより、アルカリ金属等を塩化物にし
て揮発分離することが記載されている。これら従来の精
製方法は、石英粉末に含まれるナトリウムやカリウムに
ついてはある程度の効果が得られるが、リチウムについ
ては十分な精製効果が得られない問題がある。また、塩
素ガスを用いるとその排ガス処理に手間がかかる欠点が
ある。
[0004] On the other hand, a method of purifying quartz powder using a chlorine-containing gas or the like has been conventionally known. For example,
55-42267, JP-A-62-30632, JP-A-63-100
No. 038 describes that a natural quartz powder or the like is subjected to a heat treatment in a chlorine-containing gas stream to convert an alkali metal or the like into a chloride and volatilize and separate the chloride. These conventional refining methods can provide some effect for sodium and potassium contained in quartz powder, but have a problem that sufficient refining effect cannot be obtained for lithium. Further, when chlorine gas is used, there is a disadvantage that the exhaust gas treatment is troublesome.

【0005】また、米国特許第4,956,069号公報には、
石英粉末を装入した横型回転炉に、塩素含有ガスを導入
すると共に電流を通じて石英粉末を精製する装置が記載
されている。この精製装置では装置構成の安定化を図る
ために横型キルンを用い、キルンを回転して石英粉末を
分散流動させて塩素含有ガスと接触させている。この機
械的な回転機構のために装置が大型化する傾向があり、
また、回転を妨げないように電極やガス流通の構造が回
転軸の周囲に限定されるので装置構成が複雑になる。し
かも、石英粉末とガスとの接触が必ずしも良好ではない
ために精製効果が良くない。さらに、この精製装置では
石英粉末が回転されるので電極材が石英粉末によって削
られ、これが石英粉末に混入して不純物となる問題があ
る。とくに電極材が炭化珪素(SiC)製であると、石英粉
末に混入した炭化珪素が石英溶融時に気泡を生じてルツ
ボの欠陥になる。また、本装置は塩素含有ガスを炉内に
導入してアルカリ金属を塩化物にし、揮発除去している
が、排ガスの温度が適切に維持され通気が円滑でないと
精製炉の排気口にアルカリ塩化物が凝縮して石英粉末に
混入し不純物になる虞がある。
Further, US Pat. No. 4,956,069 discloses that
An apparatus for introducing a chlorine-containing gas into a horizontal rotary furnace charged with quartz powder and purifying the quartz powder through an electric current is described. In this refining apparatus, a horizontal kiln is used in order to stabilize the configuration of the apparatus, and the kiln is rotated to disperse and flow the quartz powder to contact the chlorine-containing gas. This mechanical rotation mechanism tends to increase the size of the device,
In addition, the structure of the electrodes and the gas flow is limited around the rotating shaft so as not to hinder the rotation, so that the device configuration becomes complicated. In addition, since the contact between the quartz powder and the gas is not always good, the refining effect is not good. Further, in this refining apparatus, since the quartz powder is rotated, there is a problem that the electrode material is shaved by the quartz powder, and this is mixed with the quartz powder to become an impurity. In particular, if the electrode material is made of silicon carbide (SiC), the silicon carbide mixed in the quartz powder generates bubbles when the quartz is melted, resulting in crucible defects. In addition, this equipment introduces chlorine-containing gas into the furnace to convert alkali metals into chlorides, which are volatilized and removed. There is a possibility that the substance condenses and mixes with the quartz powder to become an impurity.

【0006】[0006]

【発明が解決しようとする課題】本発明は、従来の精製
技術における上記問題を解決するものであり、石英粉末
に含まれるアルカリ金属や銅、鉄などの不純物金属を簡
単な構成で、しかも効率よく低減することができる精製
技術を提供するものである。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems in the conventional refining technology. The present invention solves the problem of removing impurities such as alkali metals, copper, and iron contained in quartz powder with a simple structure and at a high efficiency. It is intended to provide a purification technique that can be reduced well.

【0007】[0007]

【課題を解決するための手段】すなわち本発明は、
(1)陽極と陰極との間に石英ガラス製の隔壁を設けた
精製容器を用い、隔壁の両側に装入した石英粉末に高温
下で電場を形成し、石英粉末に含有されている不純物金
属を陰極側に移動させることによって陽極側石英粉末の
不純物金属量を低減することを特徴とする石英粉末の精
製方法に関する。
That is, the present invention provides:
(1) Using a purification vessel provided with a quartz glass partition wall between the anode and the cathode, forming an electric field at high temperature on the quartz powder charged on both sides of the partition wall at a high temperature, and forming an impurity metal contained in the quartz powder. To a method for purifying quartz powder, characterized in that the amount of impurity metal in the quartz powder on the anode side is reduced by moving the powder to the cathode side.

【0008】本発明の上記精製方法は、好ましくは、
(2)窒素ガス雰囲気下、空気雰囲気下、またはこれら
に少量の水素ないし水を含む雰囲気下で、石英粉末の電
解精製を行う方法、(3)精製容器内の石英粉末に、8
00〜1300℃の高温下で、50V/cm以上の電場を形
成することによって石英粉末の電解精製を行う精製方法
(4)リチウム、カリウム、ナトリウム、銅、鉄の含有
量をおのおの0.1ppm以下に低減する精製方法、(5)
外筒の内側に内筒を有する二重管構造の石英ガラス製容
器であって、外筒の周面と内筒の内側に電極を設けた精
製容器を用い、外筒と内筒におのおの石英粉末を装入し
て精製する方法、(6)角形容器の両側に電極を有し、
内部が隔壁で仕切られた石英ガラス製の精製容器を用い
る精製方法を含む。
[0008] The purification method of the present invention preferably comprises
(2) a method of electrolytically refining quartz powder in a nitrogen gas atmosphere, an air atmosphere, or an atmosphere containing a small amount of hydrogen or water therein;
A purification method for performing electrolytic refining of quartz powder by forming an electric field of 50 V / cm or more at a high temperature of 00 to 1300 ° C. (4) The content of lithium, potassium, sodium, copper, and iron is 0.1 ppm or less in each case. Purification method to reduce to (5)
A quartz glass container having a double-tube structure having an inner tube inside the outer tube, using a purification container provided with electrodes on the peripheral surface of the outer tube and inside the inner tube, and each of the outer and inner tubes being made of quartz. A method of charging and purifying the powder, (6) having electrodes on both sides of a rectangular container,
The method includes a purification method using a purification container made of quartz glass whose inside is partitioned by partition walls.

【0009】また、本発明は、(7)石英粉末を入れる
精製容器と加熱手段とを備え、精製容器は外筒とその内
側に内筒を有する二重管構造の石英ガラス製容器であっ
て、外筒の周面と内筒の内側に電極を有し、さらに容器
内部に通じる通気路が設けられていることを特徴とする
石英粉末の精製装置、(8)角形の石英ガラス製精製容
器と加熱手段とを備え、容器の両側には電極が設けら
れ、内部が隔壁で仕切られており、さらに容器内部に通
じる通気路が設けられていることを特徴とする石英粉末
の精製装置に関する。
Further, the present invention provides (7) a purifying vessel containing quartz powder and a heating means, wherein the purifying vessel is a quartz glass vessel having a double tube structure having an outer cylinder and an inner cylinder inside thereof. An apparatus for purifying quartz powder, comprising: electrodes on the outer surface of the outer tube and the inner surface of the inner tube, and further provided with an air passage communicating with the inside of the container. And a heating means, electrodes are provided on both sides of the container, the inside is partitioned by partition walls, and an air passage leading to the inside of the container is further provided.

【0010】さらに本発明は、(9)上記(1)〜(6)の何
れかの方法によって精製された石英粉末によって製造さ
れた石英ガラス製品に関する。
[0010] The present invention further relates to (9) a quartz glass product produced from the quartz powder refined by any of the above (1) to (6).

【0011】[0011]

【発明の実施の態様】以下、本発明を実施態様に即して
詳細に説明する。図1は本発明に係る縦型筒状装置の概
略断面図、図2はその概略横断面図、図3、図4は本発
明に係る他の装置構成例を示す概略縦断面図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to embodiments. FIG. 1 is a schematic cross-sectional view of a vertical cylindrical device according to the present invention, FIG. 2 is a schematic transverse cross-sectional view thereof, and FIGS.

【0012】(I)精製方法 図示するように、本発明の精製方法は、陽極と陰極を備
え、両極の間に隔壁を設けた電解精製容器を用いる。こ
の隔壁は石英粉末から放出されたアルカリ金属等の不純
物金属イオンの移動が妨げられないように石英ガラスか
らなるものが好ましい。陽極と陰極および隔壁を有する
ものであれば精製容器の形状は限定されない。筒型でも
良く、角型でも良い。精製容器の例としては、図1,2
に示す筒状の縦型容器を用いることができる。この容器
10は外筒11と内筒12とからなる二重管の構造を有
し、内筒12が隔壁となり、外筒11の下部内周を囲む
帯状の陽極または陰極13が設けられており、これと対
になる棒状の電極14が内筒12の軸芯に設けられてい
る。
(I) Purification Method As shown in the figure, the purification method of the present invention uses an electrolytic purification vessel provided with an anode and a cathode and having a partition wall between both electrodes. The partition walls are preferably made of quartz glass so that the movement of impurity metal ions such as alkali metals released from the quartz powder is not hindered. The shape of the purification vessel is not limited as long as it has an anode, a cathode, and a partition. It may be cylindrical or square. Figures 1 and 2 show examples of purification vessels.
Can be used. The container 10 has a double-pipe structure including an outer cylinder 11 and an inner cylinder 12, the inner cylinder 12 serving as a partition wall, and a strip-shaped anode or cathode 13 surrounding the lower inner periphery of the outer cylinder 11. A pair of rod-shaped electrodes 14 is provided on the axis of the inner cylinder 12.

【0013】精製容器の他の例は、図3に示すように、
縦型の筒型容器31の上端および下端に陽極33または
陰極34を設け、この容器内部を上下に仕切る隔壁32
を設けたものでも良い。また、図4に示すように、角型
容器40の両側に陽極41または陰極42を設け、その
間に隔壁43を設けたものでも良い。陽極および陰極の
材質はカーボンまたは白金が好ましい。外筒の電極や角
型容器の電極は、石英ガラス質の容器を用いた場合、容
器の外周に電極を密着して取り付けても良い。電極を容
器の外周に装着することにより、石英粉末の流動によっ
て電極が磨耗するのを防止することができる。なお、石
英ガラス製の容器の外周に電極を設けても、電極が密着
して設けられていれば石英粉末に十分な電場をかけるこ
とができる。また、石英粉末全体に均一に電場が印加さ
れるように、電極の少なくとも一方は面状に形成したも
のが良い。
Another example of a purification vessel is shown in FIG.
An anode 33 or a cathode 34 is provided at an upper end and a lower end of a vertical cylindrical container 31, and a partition 32 that vertically partitions the inside of the container.
May be provided. Further, as shown in FIG. 4, an anode 41 or a cathode 42 may be provided on both sides of a rectangular container 40, and a partition 43 may be provided therebetween. The material of the anode and the cathode is preferably carbon or platinum. When a quartz glass container is used as the electrode of the outer cylinder or the electrode of the rectangular container, the electrode may be closely attached to the outer periphery of the container. By mounting the electrode on the outer periphery of the container, it is possible to prevent the electrode from being worn by the flow of the quartz powder. Even if electrodes are provided on the outer periphery of the quartz glass container, a sufficient electric field can be applied to the quartz powder if the electrodes are provided in close contact. It is preferable that at least one of the electrodes is formed in a planar shape so that an electric field is uniformly applied to the entire quartz powder.

【0014】電解容器の隔壁に密着するように陽極と陰
極の間に石英粉末を充填し、高温下で、上記電極を通じ
て直流電圧を印加して石英粉末に高強度の電場をかけ
る。具体的には、800〜1300℃の高温下で、50
V/cm以上、好ましくは100V/cm以上、より好ましくは
500V/cm以上の電場を加える。通電時間は石英粉末の
量に応じて調整すれば良い。なお、カーボン製の電極を
用いる場合には、電極の酸化による劣化を防止するため
容器を密閉型とし内部を窒素ガス雰囲気にするのが好ま
しい。アルゴンガスは放電を招きやすいので好ましくな
い。白金製電極等の場合には空気雰囲気で良く、容器内
部を密閉しなくても良い。
A quartz powder is filled between the anode and the cathode so as to be in close contact with the partition wall of the electrolytic vessel, and a high-voltage electric field is applied to the quartz powder at a high temperature by applying a DC voltage through the electrodes. Specifically, at a high temperature of 800 to 1300 ° C., 50
An electric field of at least V / cm, preferably at least 100 V / cm, more preferably at least 500 V / cm is applied. The energization time may be adjusted according to the amount of the quartz powder. When a carbon electrode is used, it is preferable that the container is closed and the inside is a nitrogen gas atmosphere in order to prevent deterioration of the electrode due to oxidation. Argon gas is not preferable because it easily causes discharge. In the case of a platinum electrode or the like, the atmosphere may be an air atmosphere, and the interior of the container need not be sealed.

【0015】なお、これらの窒素ガス雰囲気または空気
雰囲気に、少量の水素または水を含有させることによっ
て精製効果を高めることができる。添加量は雰囲気中の
濃度で、水素の場合1〜5wt%、水(水蒸気)の場合5〜
30wt%が好ましい。
The purification effect can be enhanced by adding a small amount of hydrogen or water to the nitrogen gas atmosphere or air atmosphere. The amount of addition is the concentration in the atmosphere, 1-5 wt% for hydrogen, 5-5 for water (steam).
30 wt% is preferred.

【0016】容器内の石英粉末に電場を加えると、石英
粉末に含まれているアルカリ金属等の不純物金属がイオ
ン化して陰極に引き寄せられる。隔壁は石英粉末と同様
に石英ガラス製であるので陽極側の石英粉末に含まれる
不純物金属イオンは隔壁を通過して陰極側に移動する。
この結果、陽極側の石英粒子に含まれる不純物金属量が
低減し、石英粉末を精製することができる。陰極側の石
英粒子にはアルカリ金属等の不純物金属イオンが濃集す
るが、陽極側と陰極側とは隔壁によって仕切られている
ので、両方の石英粉末が混じることはなく、陽極側の精
製石英粉末を陰極側の石英粉末と分離して回収すること
ができる。なお、陰極側の石英粉末は再使用することが
できる。
When an electric field is applied to the quartz powder in the container, impurity metals such as alkali metals contained in the quartz powder are ionized and attracted to the cathode. Since the partition is made of quartz glass like the quartz powder, impurity metal ions contained in the quartz powder on the anode side move to the cathode side through the partition.
As a result, the amount of impurity metal contained in the quartz particles on the anode side is reduced, and the quartz powder can be purified. Impurity metal ions such as alkali metals concentrate in the quartz particles on the cathode side, but since the anode side and the cathode side are separated by partition walls, both quartz powders are not mixed, and the purified quartz on the anode side The powder can be separated and recovered from the quartz powder on the cathode side. The quartz powder on the cathode side can be reused.

【0017】このように、本発明の上記精製方法は、石
英ガラス製の隔壁を介在させて石英粉末に電場を加える
ことにより、アルカリ金属等の不純物金属イオンがこの
隔壁を通じて陰極側に移動するので、陽極側石英粉末の
不純物金属量が低減し、優れた精製効果を得ることがで
き、かつ隔壁によって陽極側の精製石英粉末と陰極側の
石英粉末とを分離して回収することができる。
As described above, according to the above-mentioned purification method of the present invention, by applying an electric field to quartz powder through a quartz glass partition, impurity metal ions such as alkali metals move to the cathode side through the partition. In addition, the amount of impurity metal in the anode-side quartz powder is reduced, an excellent refining effect can be obtained, and the purified quartz powder on the anode side and the quartz powder on the cathode side can be separated and collected by the partition walls.

【0018】なお、塩素ガス等を用いる従来の精製方法
では特にリチウムの精製効果が低いが、本発明の精製方
法によれば、アルカリ金属が電場の作用によってイオン
化するのでリチウムについても良好な精製効果を得るこ
とができる。具体的には、リチウム、カリウムおよびナ
トリウムを何れも0.1ppm以下、好ましくは0.05ppm
以下に低減することができる。従って、本発明の方法に
よって精製した石英粉末を用いることにより、アルカリ
金属不純物が大幅に少ない石英ガラス製品を得ることが
できる。
The conventional purification method using chlorine gas or the like has a particularly low purification effect on lithium. However, according to the purification method of the present invention, since the alkali metal is ionized by the action of an electric field, the purification effect on lithium is also good. Can be obtained. Specifically, any of lithium, potassium and sodium is 0.1 ppm or less, preferably 0.05 ppm.
It can be reduced below. Therefore, by using the quartz powder purified by the method of the present invention, a quartz glass product having significantly less alkali metal impurities can be obtained.

【0019】(II)精製装置 本発明に係る図1,図2の精製装置は、図示するよう
に、石英粉末50を入れる縦型容器10とその加熱手段
(図示省略)によって形成されている。容器10は縦型の
外筒11と、その内側に一定間隔を保って設けた石英ガ
ラス質の内筒12とによって形成されており、この外筒
11と内筒12からなる二重管構造を有している。外筒
11と内筒12は石英ガラス製のものを用いることがで
きる。石英ガラス製の外筒および内筒を用い、この外筒
周壁と内筒内側におのおの電極を設けることにより、石
英粉末全体に効果的に電場をかけることができる。具体
的には、外筒11の周面にはカーボン製の陽極13が外
筒の内周を巡って設けられており、一方、内筒12の中
央には棒状の陰極14が設けられている。外筒11およ
び内筒12の頭部にはおのおの蓋15,16が冠着し、
内筒12は倒れないように外筒11の蓋15によって支
えられている。これら外筒11および内筒12の内部は
蓋15,16によって密閉されている。この蓋15,16
にはおのおの石英粉末を内部に供給する開口部21,2
2が設けられている。また、外筒11の底部は通気性の
床材17によって形成されており、その下側に通気室1
8が形成されている。通気室18には通気路20が接続
しており、この通気路20に対応して上記蓋15には排
気管路19が接続している。なお、通気室18を設けず
に通気路20を直接に外筒の底部に接続しても良い。
(II) Refining Apparatus The refining apparatus shown in FIGS. 1 and 2 according to the present invention comprises, as shown in FIG.
(Not shown). The container 10 is formed by a vertical outer cylinder 11 and a quartz glass inner cylinder 12 provided at a constant interval inside the outer cylinder 11, and has a double tube structure composed of the outer cylinder 11 and the inner cylinder 12. Have. The outer cylinder 11 and the inner cylinder 12 can be made of quartz glass. An electric field can be effectively applied to the entire quartz powder by using an outer cylinder and an inner cylinder made of quartz glass and providing electrodes on the outer peripheral wall and inside of the inner cylinder. Specifically, an anode 13 made of carbon is provided on the peripheral surface of the outer cylinder 11 around the inner periphery of the outer cylinder, while a rod-shaped cathode 14 is provided at the center of the inner cylinder 12. . Lids 15, 16 are crowned on the heads of the outer cylinder 11 and the inner cylinder 12, respectively.
The inner cylinder 12 is supported by the lid 15 of the outer cylinder 11 so as not to fall down. The insides of the outer cylinder 11 and the inner cylinder 12 are sealed by lids 15 and 16. These lids 15, 16
Have openings 21 and 2 for supplying quartz powder inside
2 are provided. Further, the bottom of the outer cylinder 11 is formed of a permeable flooring material 17, and the ventilation chamber 1
8 are formed. A ventilation path 20 is connected to the ventilation chamber 18, and an exhaust pipe 19 is connected to the lid 15 corresponding to the ventilation path 20. The ventilation path 20 may be directly connected to the bottom of the outer cylinder without providing the ventilation chamber 18.

【0020】外筒11および内筒12の内部に石英粉末
を陽極13の高さに充填し、この石英粉末を充填した容
器内部に、カーボン製電極を保護するために窒素ガスを
導入し、外筒11の周囲に配設したヒータ(図示省略)に
よって容器内部を800〜1300℃に加熱し、電極1
3,14を通じて石英粉末に50V/cm以上、好ましくは
500V/cm以上の電場を加える。なお、白金製電極を用
いた場合には容器内部に窒素ガスを導入する必要はな
い。
A quartz powder is filled into the outer cylinder 11 and the inner cylinder 12 at the height of the anode 13, and a nitrogen gas is introduced into the vessel filled with the quartz powder to protect the carbon electrode. The inside of the vessel is heated to 800 to 1300 ° C. by a heater (not shown)
An electric field of 50 V / cm or more, preferably 500 V / cm or more is applied to the quartz powder through 3, 14. When a platinum electrode is used, it is not necessary to introduce nitrogen gas into the container.

【0021】電場の作用により、外筒11と内筒12の
間に充填されている石英粉末に含まれるアルカリ金属等
の不純物金属はイオン化し、内筒12を通過して陰極側
に移動し内筒12の内側に濃集する。この結果、外筒側
の石英粒子の不純物金属量が低減する。精製後、蓋15
を外して外筒側の精製した石英粉末50を取り出す。一
方、内筒12の石英粉末50は、引き続き内筒に充填し
たまま外筒側に新たな石英粉末を充填して電解精製を継
続してもよく、あるいは内筒の石英粉末を取り出して新
たな石英粉末と混合し、再利用しても良い。
Due to the action of the electric field, impurity metals such as alkali metals contained in the quartz powder filled between the outer cylinder 11 and the inner cylinder 12 are ionized, move through the inner cylinder 12 to the cathode side, and move to the cathode side. It concentrates inside the cylinder 12. As a result, the amount of impurity metal in the quartz particles on the outer cylinder side is reduced. After purification, lid 15
And take out the purified quartz powder 50 on the outer cylinder side. On the other hand, the quartz powder 50 in the inner cylinder 12 may be filled with new quartz powder in the outer cylinder while continuing to fill the inner cylinder, and electrolytic refining may be continued. It may be mixed with quartz powder and reused.

【0022】図3に示す装置構成は、縦型容器31の内
部を隔壁32で上下に仕切ったものであり、筒状容器3
1の底部に陽極34と排出口35が設けられており、一
方、容器31の頭部には蓋37が冠着し、この蓋37に
陰極33が設けられている。上記隔壁32は石英ガラス
によって形成されており容器内部に遊嵌されている。な
お、容器底部に陰極を設け頭部に陽極を設けても良い。
The apparatus configuration shown in FIG. 3 is such that the inside of a vertical container 31 is vertically divided by a partition wall 32, and a cylindrical container 3 is provided.
An anode 34 and a discharge port 35 are provided at the bottom of the container 1, while a lid 37 is mounted on the head of the container 31, and a cathode 33 is provided on the lid 37. The partition 32 is made of quartz glass and is loosely fitted inside the container. Note that a cathode may be provided at the bottom of the container and an anode may be provided at the head.

【0023】容器31の蓋37を開けて内部に石英粉末
を頭部付近まで装入した後に、隔壁32を石英粉末に載
せ、さらにその上に石英粉末を入れて蓋37を閉める。
次いで、電極33,34を通じて電圧を印加し、石英粉
末に電場を加える。この電場の作用により、陽極側の石
英粉末のアルカリ金属量が低減する。通電停止後、排出
口35を開いて容器内部の石英粉末を取り出す。陽極側
の精製された石英粉末50が排出口35から抜き出され
るのに伴って隔壁32が自重によって次第に下降し、精
製石英粉末の排出終了と共に排出口35を塞ぎ、陰極側
の石英粉末が容器内部に残る。
After the lid 37 of the container 31 is opened and the quartz powder is charged into the vicinity of the head, the partition wall 32 is placed on the quartz powder, the quartz powder is put thereon, and the lid 37 is closed.
Next, a voltage is applied through the electrodes 33 and 34 to apply an electric field to the quartz powder. The action of this electric field reduces the amount of alkali metal in the quartz powder on the anode side. After stopping the power supply, the discharge port 35 is opened to take out the quartz powder inside the container. As the purified quartz powder 50 on the anode side is extracted from the outlet 35, the partition wall 32 gradually descends by its own weight, and closes the outlet 35 when the discharge of the purified quartz powder is completed. Remains inside.

【0024】図4の装置構成は、角型容器40を用いた
ものであり、容器40の両側面に陽極41と陰極42が
設けられており、これらの間に石英ガラス質の隔壁43
が介設されている。容器40の上面は蓋44によって閉
じられている。陽極41と陰極42および隔壁43に接
触するように容器内部に石英粉末50を充填する。この
石英粉末50に電場を加えることにより、陽極側の石英
粉末の不純物金属量を低減することができる。
The apparatus shown in FIG. 4 uses a rectangular container 40. An anode 41 and a cathode 42 are provided on both sides of the container 40.
Is interposed. The upper surface of the container 40 is closed by a lid 44. The inside of the container is filled with quartz powder 50 so as to be in contact with the anode 41, the cathode 42 and the partition 43. By applying an electric field to the quartz powder 50, the amount of impurity metals in the quartz powder on the anode side can be reduced.

【0025】(III)精製例 図1,図2に示す装置構成の精製装置を用い、石英粉末
20kgを容器(外筒および内筒)に充填し、カーボン製電
極を保護するため容器内部に窒素ガスを導入した後に1
200℃に加熱し、石英粉末に15kvの直流電圧を6時
間印加した。この電解精製後、石英粉末に含まれるリチ
ウム、ナトリウム、カリウムの濃度を定量した。この結
果を表1のNo.1に示した。処理前の石英粉末に比較し
て、外筒側の石英粉末(20kg)のアルカリ金属濃度は大幅
に低減しており、特にリチウムは0.01ppmと約1/2
0に激減している。また、ナトリウム、カリウムの濃度
も0.1ppm以下であり、優れた精製効果が得られた。一
方、内筒側の石英粉末(20kg)のアルカリ金属量は増加し
ており、外筒側の石英粉末に含まれるアルカリ金属が内
筒側の石英粉末に移動して濃集したことが分かる。
(III) Purification Example Using a purification apparatus having the apparatus configuration shown in FIGS. 1 and 2, 20 kg of quartz powder was charged into a vessel (outer cylinder and inner cylinder), and nitrogen was placed inside the vessel to protect the carbon electrode. 1 after introducing gas
The mixture was heated to 200 ° C., and a DC voltage of 15 kv was applied to the quartz powder for 6 hours. After this electrolytic purification, the concentrations of lithium, sodium, and potassium contained in the quartz powder were quantified. The results are shown in Table 1 No. 1. Compared with the quartz powder before the treatment, the alkali metal concentration of the quartz powder (20 kg) on the outer cylinder side is greatly reduced, and especially lithium is 0.01 ppm, which is about 1/2.
It has dropped sharply to zero. In addition, the concentrations of sodium and potassium were 0.1 ppm or less, and an excellent purification effect was obtained. On the other hand, the amount of alkali metal in the quartz powder (20 kg) on the inner cylinder side is increasing, and it can be seen that the alkali metal contained in the quartz powder on the outer cylinder moved to and concentrated on the quartz powder on the inner cylinder side.

【0026】電圧の印加時間を3時間に変え、容器内の
雰囲気を窒素ガス雰囲気(No.2)、水素2wt%混入した
窒素ガス雰囲気(No.3)、水蒸気15wt%を混入した窒
素ガス雰囲気(No.4)に変えた以外は上記と同様にして
石英粉末を電解精製した。この結果を表1に示した。こ
の結果に示すように、窒素ガスに少量の水素または水蒸
気を混入することによって、精製効果が大幅に向上する
ことが確認された。すなわち、No.3〜4の精製時間はN
o.1の1/2であるが、アルカリ金属、銅、鉄についてN
o.1の場合を上回る除去効果を達成している。
The voltage application time was changed to 3 hours, and the atmosphere in the container was a nitrogen gas atmosphere (No. 2), a nitrogen gas atmosphere (No. 3) mixed with 2 wt% of hydrogen, and a nitrogen gas atmosphere mixed with 15 wt% of steam. (No. 4), except that the quartz powder was electrolytically purified in the same manner as above. The results are shown in Table 1. As shown in the results, it was confirmed that the refining effect was significantly improved by mixing a small amount of hydrogen or steam into the nitrogen gas. That is, the purification time of Nos. 3 to 4 was N
o. 1/2 of alkali metal, copper and iron
o.1 Achieved a greater removal effect than the case of 1.

【0027】[0027]

【表1】 [Table 1]

【0028】[0028]

【発明の効果】本発明の精製方法および精製装置によれ
ば、石英粉末に含有されているアルカリ金属や銅、鉄な
どの不純物金属を簡単な構成で、しかも効率良く低減す
ることができる。
According to the refining method and the refining apparatus of the present invention, impurity metals such as alkali metal, copper, and iron contained in quartz powder can be reduced efficiently with a simple structure.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明に係る型筒状装置の概略縦断面図FIG. 1 is a schematic longitudinal sectional view of a cylindrical device according to the present invention.

【図2】 図1に示す装置の概略横断面図FIG. 2 is a schematic cross-sectional view of the apparatus shown in FIG.

【図3】 本発明に係る他の装置構成例を示す概略縦断
面図
FIG. 3 is a schematic longitudinal sectional view showing another example of the device configuration according to the present invention.

【図4】 本発明に係る他の装置構成例を示す概略縦断
面図
FIG. 4 is a schematic longitudinal sectional view showing another example of the device configuration according to the present invention.

【符号の説明】[Explanation of symbols]

10−精製装置、11−外筒、12−内筒、13−陽
極、14−陰極、15,16−蓋、17−床材、18−通
気室、19−排気管路、20−通気路、21,22−開
口部、31−容器、32−隔壁、33−陰極、34−陽
極、35−排出口、37−蓋、40−容器、41−陽
極、42−陰極、43−隔壁、44−蓋
10-refiner, 11-outer cylinder, 12-inner cylinder, 13-anode, 14-cathode, 15,16-lid, 17-floor, 18-vent room, 19-exhaust line, 20-vent line, 21, 22-opening, 31-container, 32-partition, 33-cathode, 34-anode, 35-discharge, 37-lid, 40-container, 41-anode, 42-cathode, 43-partition, 44- lid

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 陽極と陰極との間に石英ガラス製の隔壁
を設けた精製容器を用い、隔壁の両側に装入した石英粉
末に高温下で電場を形成し、石英粉末に含有されている
不純物金属を陰極側に移動させることによって陽極側石
英粉末の不純物金属量を低減することを特徴とする石英
粉末の精製方法。
1. A purification vessel having a quartz glass partition wall between an anode and a cathode is used. An electric field is formed at a high temperature on the quartz powder charged on both sides of the partition wall, and the quartz powder is contained in the quartz powder. A method for purifying quartz powder, comprising reducing the amount of impurity metal in the quartz powder on the anode side by moving the impurity metal to the cathode side.
【請求項2】 窒素ガス雰囲気下、空気雰囲気下、また
はこれらに少量の水素ないし水を含む雰囲気下で、石英
粉末の電解精製を行う請求項1の精製方法。
2. The method according to claim 1, wherein the quartz powder is electrorefined in a nitrogen gas atmosphere, an air atmosphere, or an atmosphere containing a small amount of hydrogen or water.
【請求項3】 精製容器内の石英粉末に、800〜13
00℃の高温下で、50V/cm以上の電場を形成すること
によって石英粉末の電解精製を行う請求項1または2の
精製方法。
3. The method according to claim 1, wherein the quartz powder in the refining vessel contains 800 to 13 particles.
The method according to claim 1 or 2, wherein the quartz powder is subjected to electrolytic refining by forming an electric field of 50 V / cm or more at a high temperature of 00 ° C.
【請求項4】 リチウム、カリウム、ナトリウム、銅、
鉄の含有量をおのおの0.1ppm以下に低減する請求項
1,2または3の精製方法。
4. Lithium, potassium, sodium, copper,
4. The method according to claim 1, wherein the iron content is reduced to 0.1 ppm or less.
【請求項5】 外筒の内側に内筒を有する二重管構造の
石英ガラス製容器であって、外筒の周面と内筒の内側に
電極を設けた精製容器を用い、外筒と内筒におのおの石
英粉末を装入して精製する請求項1の精製方法。
5. A quartz glass container having a double tube structure having an inner cylinder inside an outer cylinder, wherein a purification vessel having a peripheral surface of the outer cylinder and electrodes provided inside the inner cylinder is used. 2. The refining method according to claim 1, wherein quartz powder is charged into the inner cylinder for purification.
【請求項6】 角形容器の両側に電極を有し、内部が隔
壁で仕切られた石英ガラス製の精製容器を用いる請求項
1の精製方法。
6. The refining method according to claim 1, wherein an electrode is provided on both sides of the rectangular container, and a refining container made of quartz glass is used.
【請求項7】 石英粉末を入れる精製容器と加熱手段と
を備え、精製容器は外筒とその内側に内筒を有する二重
管構造の石英ガラス製容器であって、外筒の周面と内筒
の内側に電極を有し、さらに容器内部に通じる通気路が
設けられていることを特徴とする石英粉末の精製装置。
7. A refining vessel for holding quartz powder and a heating means, wherein the refining vessel is a quartz glass vessel having a double tube structure having an outer cylinder and an inner cylinder inside thereof, wherein the outer peripheral cylinder has a peripheral surface. An apparatus for purifying quartz powder, comprising: an electrode inside an inner cylinder; and a ventilation path communicating with the inside of the container.
【請求項8】 角形の石英ガラス製精製容器と加熱手段
とを備え、容器の両側には電極が設けられ、内部が隔壁
で仕切られており、さらに容器内部に通じる通気路が設
けられていることを特徴とする石英粉末の精製装置。
8. A prismatic quartz glass refining container and a heating means are provided, electrodes are provided on both sides of the container, the inside is partitioned by partition walls, and an air passage leading to the inside of the container is provided. An apparatus for refining quartz powder.
【請求項9】 請求項1〜6の何れかの方法によって精
製された石英粉末によって製造された石英ガラス製品。
9. A quartz glass product produced from quartz powder refined by the method according to claim 1.
JP2001019768A 2000-03-17 2001-01-29 Method and apparatus for refining quartz powder and quartz glass product Expired - Fee Related JP4557441B2 (en)

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JP2000075149 2000-03-17
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007049811A1 (en) * 2005-10-28 2007-05-03 Japan Super Quartz Corporation Method for purification of silica particles, purifier, and purified silica particles
KR101081834B1 (en) 2003-04-02 2011-11-09 쟈판 스파 쿼츠 가부시키가이샤 High purity silica glass crucible by electrolytic refining, and its production method and pulling method
CN110127708A (en) * 2019-05-01 2019-08-16 黄冈师范学院 A kind of SiO2Purity >=99.99% glass sand method of purification

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101081834B1 (en) 2003-04-02 2011-11-09 쟈판 스파 쿼츠 가부시키가이샤 High purity silica glass crucible by electrolytic refining, and its production method and pulling method
WO2007049811A1 (en) * 2005-10-28 2007-05-03 Japan Super Quartz Corporation Method for purification of silica particles, purifier, and purified silica particles
US7935326B2 (en) 2005-10-28 2011-05-03 Japan Super Quartz Corporation Method for purification of silica particles, purifier, and purified silica particles
US8506890B2 (en) 2005-10-28 2013-08-13 Japan Super Quartz Corporation Method for purification of silica particles, purifier, and purified silica particles
CN110127708A (en) * 2019-05-01 2019-08-16 黄冈师范学院 A kind of SiO2Purity >=99.99% glass sand method of purification
CN110127708B (en) * 2019-05-01 2021-09-03 黄冈师范学院 Method for purifying high-purity quartz sand with purity of SiO2 being more than or equal to 99.99 percent

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